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Ship safety and fire fighting

Marine Engineering (B.E./B.Tech) · Ship and safety · free study notes for exams, placements and interviews

In short

Ship safety and fire fighting covers how fire is prevented, detected, contained and extinguished on board, and how crew and passengers are protected and evacuated when prevention fails. A ship is an isolated steel box with large fuel oil quantities, hot surfaces, confined spaces and no fire brigade to call, so statutory requirements are unusually prescriptive — SOLAS Chapter II-2 (fire), Chapter III (life-saving appliances) with the LSA Code, the FSS Code and the ISM Code. In India these are enforced through the Merchant Shipping Act, 2025 (in force 15 March 2026; it repealed the 1958 Act) and rules made under it, administered by the Directorate General of Shipping (DG Shipping, renamed the Directorate General of Maritime Administration, DGMA, in 2026) and recognised classification societies such as the Indian Register of Shipping. The topic is examined in marine engineering ship safety / fire fighting papers, in the DG Shipping competency examinations and STCW mandatory courses (Basic and Advanced Fire Fighting, Personal Survival Techniques), and is asked in almost every interview for sea-going and shipyard jobs with SCI, Great Eastern Shipping, Essar, Synergy, Anglo-Eastern, Fleet, Cochin Shipyard and Mazagon Dock.

Explained

Fire theory and classification

Fire prevention and structural protection

Detection and alarm

Portable and fixed fire fighting systems

Life-saving appliances and emergency response

Indian statutory framework and management systems

Key points

Formulas and examples

CO₂ mass required, W = ρ_CO₂ × C × V, where V = gross volume of the protected space (m³), C = design concentration as a volume fraction (0.40 machinery spaces, 0.30 cargo holds) and ρ_CO₂ ≈ 1.80 kg/m³ of free gas at 15 °C (specific volume 0.56 m³/kg). Cylinders are 45 kg nominal, so number of cylinders N = W / 45, rounded up.
Theoretical oxygen dilution: O₂% after flooding = 21 × (1 − C). Volume of CO₂ to reach a target O₂ fraction: C = 1 − (O₂ target / 21).
Fire pump capacity (SOLAS/FSS): total main pump capacity Q ≥ 4/3 × Q_bilge, and each hydrant jet must give a throw with nozzle pressure at least 0.27 N/mm² (cargo ships ≥ 6,000 GT: 0.27; smaller: 0.25 N/mm²). Emergency pump ≥ 40% of total main pump capacity and not less than 25 m³/h.
Hydrant discharge, Q = Cd × A × √(2 p / ρ), with A = nozzle area (m²), p = nozzle pressure (Pa), ρ = 1,000 kg/m³ for sea water (take 1,025 kg/m³ for accuracy), Cd ≈ 0.97 for a smooth nozzle. Q in m³/s; × 3,600 for m³/h.
Foam requirement (deck foam, tankers — SOLAS II-2/10.8 and FSS Code Ch. 14): solution rate R = max(0.6 L/min·m² × tank deck area, 6 L/min·m² × horizontal sectional area of the largest single tank, 3 L/min·m² × area protected by the largest monitor but never less than 1,250 L/min), supplied for at least 20 minutes on tankers fitted with an inert gas system (30 minutes if not); concentrate = R × duration × induction ratio (3% or 6%).
Heat absorbed by water cooling: Q = m c ΔT + m L, c = 4.18 kJ/kg·K, latent heat of vaporisation L = 2,257 kJ/kg at 100 °C — showing why water fog (which evaporates) absorbs far more heat than a solid jet.

Example 1 — CO₂ charge for an engine room. Engine room 18 m long × 16 m wide × 9 m high, plus casing 6 m × 5 m × 7 m.

Example 2 — hydrant jet flow and pump sizing. A 19 mm nozzle at 0.27 N/mm² (2.7 bar = 2.7 × 10⁵ Pa), sea water ρ = 1,025 kg/m³, Cd = 0.97.

Example 3 — deck foam for a crude oil tanker. Tank deck area 160 m × 32 m = 5,120 m²; largest cargo tank 32 m × 30 m = 960 m².

Example 4 — cooling power of water. A hose delivers 379 L/min (Example 2) of sea water at 28 °C onto a Class A fire.

Example 5 — inerting a cargo tank. A 12,000 m³ tank at 21% oxygen is to be inerted to 5% using inert gas containing 2% oxygen, assuming perfect dilution (mixing) and a dilution factor of about 2.5 tank volumes for the practical case.

SystemMechanismTypical spaceKey limitation
Water jet/fogCooling (plus smothering as steam)Accommodation, Class AConducts electricity; free surface and stability risk
Foam (low expansion)Smothering, sealing vapourTanker deck, fuel spillsDestroyed by heat and fuel washing; not on electrics
High-expansion foamVolume filling, smotheringMachinery space, pump roomNeeds air supply arrangement; poor visibility
CO₂ total floodingOxygen dilutionEngine room, holds, pump roomLethal to occupants; no cooling, so re-ignition risk
Dry chemical powderChain reaction inhibitionGas fires, deck, electricsNo cooling; heavy clean-up; shields visibility
Water mistCooling, local smotheringLocal application, accommodationNeeds high pressure; obstructions reduce effect
Wet chemicalSaponification of fatGalley deep fryerClass F only
Inert gasPrevention, O₂ below 8%Tanker cargo tanksAsphyxiant; corrosion and scrubber maintenance

Where it is used

Interview questions

Common mistakes

Related topics

Ship construction and stability · Naval architecture basics · Engine room watchkeeping · Marine auxiliary machinery: pumps and compressors · Marine pollution prevention and MARPOL · Industrial safety, risk assessment and HAZOP

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